{"id":356332,"date":"2024-03-11T11:49:42","date_gmt":"2024-03-11T11:49:42","guid":{"rendered":"\/forum\/forums\/reply\/356332\/"},"modified":"2024-03-11T11:49:42","modified_gmt":"2024-03-11T11:49:42","slug":"356332","status":"publish","type":"reply","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/356332\/","title":{"rendered":"Reply To: Condensation in Shell and tube heat exchanger"},"content":{"rendered":"<p>&lt;p&gt;If the liquid fraction is too low to show why is the VOF model a good choice?&nbsp;&lt;\/p&gt;&lt;p&gt;You currently have two distinct fluid domains, and that can make convergence tricky. If you remove the water domain, but set a boundary condition on the water surfaces to reflect the cooling you simplify the model and reduce the cell count.&nbsp;&lt;\/p&gt;<\/p>\n","protected":false},"template":"","class_list":["post-356332","reply","type-reply","status-publish","hentry"],"aioseo_notices":[],"acf":[],"_links":{"self":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/replies\/356332","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/replies"}],"about":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/types\/reply"}],"version-history":[{"count":0,"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/replies\/356332\/revisions"}],"wp:attachment":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/media?parent=356332"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}